2017
DOI: 10.1007/s11144-017-1164-4
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Oligomerization of 1-decene over sulfated alumina catalysts for the production of synthetic fuels and lubricants: modelling and verification

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Cited by 6 publications
(5 citation statements)
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“…The differences in the activity results of all test zeolites are related to their specific surface areas, pore size, and framework structure. Among the three zeolites, USY contained the largest pore volume, pore diameter, and a cage-like framework, which provided a more effective internal diffusion of reactant and oligomer products, resulting in higher selectivity for trimers and heavier hydrocarbons. , This was confirmed by our previous work on the oligomerization of 1-decene over sulfated alumina . The spent zeolite catalysts after 4 h of the reaction turned from white to very dark brown color, especially for USY zeolite catalyst, indicating the formation of hard coke in the catalyst pores …”
Section: Resultssupporting
confidence: 73%
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“…The differences in the activity results of all test zeolites are related to their specific surface areas, pore size, and framework structure. Among the three zeolites, USY contained the largest pore volume, pore diameter, and a cage-like framework, which provided a more effective internal diffusion of reactant and oligomer products, resulting in higher selectivity for trimers and heavier hydrocarbons. , This was confirmed by our previous work on the oligomerization of 1-decene over sulfated alumina . The spent zeolite catalysts after 4 h of the reaction turned from white to very dark brown color, especially for USY zeolite catalyst, indicating the formation of hard coke in the catalyst pores …”
Section: Resultssupporting
confidence: 73%
“…62,63 This was confirmed by our previous work on the oligomerization of 1decene over sulfated alumina. 64 The spent zeolite catalysts after 4 h of the reaction turned from white to very dark brown color, especially for USY zeolite catalyst, indicating the formation of hard coke in the catalyst pores. 65 Three feedstocks with different compositions of 1-decene, 1decanol, and internal olefins were used for the oligomerization reaction to evaluate their effects on catalytic activity and product loss via the cracking reaction.…”
Section: T H Imentioning
confidence: 97%
“…Long chain alkenes, especially 1-decene can be used to produce synthetic lubricant base stock. 1-Decene can be prepared from 1-decanol derived from the hydrogenation of fatty acids of renewable vegetable oils [1]. 1-Decene is also in a liquid state and much easier to handle compared with ethylene gas.…”
Section: Introductionmentioning
confidence: 99%
“…In Lewis acid catalysis, oligomerization is activated by a hydrogen donor agent such as water, called cationic oligomerization [3]. Other agents for oligomerization include heterogeneous acid catalysts such as sulfatedalumina [1], tungsten-zirconia [4] and zeolite [5] that are cheaper than other types of catalysts. One important feature of zeolite catalysts is that their inner structure can be manipulated to tailor products [6,7], while spent zeolite catalysts can be simply regenerated via chemical or thermal treatment [8].…”
Section: Introductionmentioning
confidence: 99%
“…The foresaid catalysts are classified in the category of the heterogeneous acid catalysts. According to the determined mechanism for oligomerization of olefins with heterogeneous acid catalysts, the reaction is initiated when olefin molecules are transformed to carbenium ions on Brønsted acid sites and further combine with olefin molecules in the bulk solution to form larger molecules . Huang and coworkers synthesized 1‐decene‐based lubricants by employing Ziegler‐Natta catalyst and silica as a support.…”
Section: Introductionmentioning
confidence: 99%